JP7322545B2 - Gas concentration adjusting agent for culturing anaerobic bacteria and method for culturing anaerobic bacteria using the same - Google Patents
Gas concentration adjusting agent for culturing anaerobic bacteria and method for culturing anaerobic bacteria using the same Download PDFInfo
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Description
本発明は、嫌気性細菌培養用ガス濃度調整剤及びこれを用いた嫌気性細菌の培養方法に関する。 The present invention relates to a gas concentration adjusting agent for culturing anaerobic bacteria and a method for culturing anaerobic bacteria using the same.
生物、生殖又はバイオテクノロジーの研究分野又は産業分野において実施される組織・細胞のような生物試料の培養では大気雰囲気と異なるガス環境が必要とされる。例えば、重炭酸塩緩衝系培養液のpHを血液の通常状態と同じpH7.4に保持するための条件として、雰囲気二酸化炭素濃度を5%程度にすることが必要である。また、多くの研究分野で、生体内と同様の低濃度酸素雰囲気下での細胞培養が行われている。 Cultivation of biological specimens such as tissues and cells performed in research fields or industrial fields of organisms, reproduction or biotechnology requires a gas environment different from the air atmosphere. For example, as a condition for maintaining the pH of the bicarbonate-buffered culture solution at pH 7.4, which is the same as the normal state of blood, it is necessary to set the atmospheric carbon dioxide concentration to about 5%. In addition, in many research fields, cell culture is performed under a low-concentration oxygen atmosphere similar to that in vivo.
高濃度二酸化炭素雰囲気及び低濃度酸素雰囲気のガス環境を作り出す手段としては、炭酸ガスインキュベーター等が知られているが、設備コストや高圧ガス管理等の負担が大きい。そのため、近年は、アスコルビン酸類の酸化反応を利用したガス濃度調整剤を用いる方法が広く利用されている(特許文献1及び2を参照)。 Carbon dioxide gas incubators and the like are known as means for creating a gas environment with a high-concentration carbon dioxide atmosphere and a low-concentration oxygen atmosphere. Therefore, in recent years, a method using a gas concentration adjusting agent that utilizes an oxidation reaction of ascorbic acids has been widely used (see Patent Documents 1 and 2).
嫌気性細菌の培養においては、高濃度二酸化炭素雰囲気のガス環境を作り出すことが要求されている。そのため、アスコルビン酸類の酸化反応において、より効率的に二酸化炭素発生量を増加することが望まれる。
本発明が解決しようとする課題は、二酸化炭素発生量が多い嫌気性細菌培養用ガス濃度調整剤を提供することである。
In culturing anaerobic bacteria, it is required to create a gas environment with a high-concentration carbon dioxide atmosphere. Therefore, it is desired to more efficiently increase the amount of carbon dioxide generated in the oxidation reaction of ascorbic acids.
The problem to be solved by the present invention is to provide a gas concentration adjusting agent for anaerobic bacteria culture that generates a large amount of carbon dioxide.
本発明者は、鋭意検討を重ねた結果、アスコルビン酸類を配合した場合に比べてデヒドロアスコルビン酸を配合した方が、二酸化炭素発生量が増加することを見出した。本発明はこのような知見に基づき完成に至ったものである。 As a result of intensive studies, the present inventors have found that the amount of carbon dioxide generated increases when dehydroascorbic acid is blended, as compared to when ascorbic acids are blended. The present invention has been completed based on such findings.
すなわち本発明は、以下に関する。
<1> (a)デヒドロアスコルビン酸、(c)遷移金属触媒、(d)活性炭、(e)アルカリ金属炭酸塩、アルカリ金属水酸化物及びアルカリ土類金属水酸化物からなる群より選ばれる少なくとも1種、並びに(f)水を含む、嫌気性細菌培養用ガス濃度調整剤。
<2> (b)アスコルビン酸類を更に含む、上記<1>に記載の嫌気性細菌培養用ガス濃度調整剤。
<3> (b)アスコルビン酸類と(a)デヒドロアスコルビン酸とのモル比[(b)/(a)]が1.5以下である、上記<2>に記載の嫌気性細菌培養用ガス濃度調整剤。
<4> 上記<1>~<3>のいずれか1つに記載のガス濃度調整剤の存在下で嫌気性細菌を培養する、嫌気性細菌の培養方法。
<5> 上記<1>~<3>のいずれか1つに記載のガス濃度調整剤を通気性包装材で小袋状に包装したガス濃度調整剤包装体。
That is, the present invention relates to the following.
<1> At least selected from the group consisting of (a) dehydroascorbic acid, (c) transition metal catalyst, (d) activated carbon, (e) alkali metal carbonate, alkali metal hydroxide and alkaline earth metal hydroxide 1, and (f) a gas concentration adjusting agent for anaerobic bacteria culture containing water.
<2> (b) The gas concentration adjusting agent for anaerobic bacteria culture according to <1> above, further comprising ascorbic acids.
<3> The gas concentration for anaerobic bacteria culture according to <2> above, wherein the molar ratio [(b)/(a)] of (b) ascorbic acids and (a) dehydroascorbic acid is 1.5 or less. regulator.
<4> A method for culturing anaerobic bacteria, comprising culturing anaerobic bacteria in the presence of the gas concentration adjusting agent according to any one of <1> to <3> above.
<5> A gas concentration adjusting agent package in which the gas concentration adjusting agent according to any one of the above <1> to <3> is packaged in a small bag with an air-permeable packaging material.
本発明の嫌気性細菌培養用ガス濃度調整剤は、二酸化炭素発生量が多く、効率的に高濃度二酸化炭素雰囲気及び低濃度酸素雰囲気のガス環境を作り出すことができる。 The gas concentration adjusting agent for anaerobic bacteria culture of the present invention generates a large amount of carbon dioxide, and can efficiently create a gas environment with a high-concentration carbon dioxide atmosphere and a low-concentration oxygen atmosphere.
以下、本発明の一実施形態について説明する。本発明の内容は以下に説明する実施形態に限定されるものではない。
なお、本明細書において、数値の記載に関する「A~B」という用語は、「A以上B以下」(A<Bの場合)又は「A以下B以上」(A>Bの場合)を意味する。また、本発明において、好ましい態様の組み合わせは、より好ましい態様である。
An embodiment of the present invention will be described below. The content of the present invention is not limited to the embodiments described below.
In this specification, the term "A to B" regarding numerical values means "A or more and B or less" (when A<B) or "A or less than B" (when A>B). . Moreover, in the present invention, a combination of preferred aspects is a more preferred aspect.
[ガス濃度調整剤]
本発明の嫌気性細菌培養用ガス濃度調整剤は、(a)デヒドロアスコルビン酸、(c)遷移金属触媒、(d)活性炭、(e)アルカリ金属炭酸塩、アルカリ金属水酸化物及びアルカリ土類金属水酸化物からなる群より選ばれる少なくとも1種、並びに(f)水を含む。ガス濃度調整剤は(b)アスコルビン酸類を更に含んでもよい。
また、本発明のガス濃度調整剤は、(a)デヒドロアスコルビン酸、(c)遷移金属触媒、(d)活性炭、(e)アルカリ金属炭酸塩、アルカリ金属水酸化物及びアルカリ土類金属水酸化物からなる群より選ばれる少なくとも1種、並びに(f)水を含む組成物を通気性包装材で包装した包装体として用いられることが好ましい。該組成物は(b)アスコルビン酸類を更に含んでもよい。
本発明のガス濃度調整剤は、(a)~(f)成分を合計で、好ましくは50質量%以上、より好ましくは60質量%以上、更に好ましくは70質量%以上含む。
[Gas concentration adjuster]
The gas concentration adjusting agent for culturing anaerobic bacteria of the present invention comprises (a) dehydroascorbic acid, (c) transition metal catalyst, (d) activated carbon, (e) alkali metal carbonate, alkali metal hydroxide and alkaline earth. It contains at least one selected from the group consisting of metal hydroxides and (f) water. The gas concentration adjusting agent may further contain (b) ascorbic acids.
Further, the gas concentration adjusting agent of the present invention includes (a) dehydroascorbic acid, (c) transition metal catalyst, (d) activated carbon, (e) alkali metal carbonate, alkali metal hydroxide and alkaline earth metal hydroxide. It is preferably used as a package in which a composition containing at least one selected from the group consisting of substances and (f) water is packaged with an air-permeable packaging material. The composition may further comprise (b) ascorbic acids.
The gas concentration adjusting agent of the present invention contains components (a) to (f) in a total amount of preferably 50% by mass or more, more preferably 60% by mass or more, and still more preferably 70% by mass or more.
(a)デヒドロアスコルビン酸
本発明のガス濃度調整剤は、酸素吸収反応の主剤として酸素吸収能及び炭酸ガス発生能を併せ持つデヒドロアスコルビン酸を含む。
デヒドロアスコルビン酸は、アスコルビン酸が酸化された化合物であり、加水分解によりジケトグロン酸を生成する。そして、適切な触媒及び反応環境を調整することにより、脱炭酸反応と酸化反応を繰り返して、二酸化炭素を発生するとともに酸素を吸収する。デヒドロアスコルビン酸は、アスコルビン酸類を酸化して生成させることもできる。
(a) Dehydroascorbic acid The gas concentration adjusting agent of the present invention contains dehydroascorbic acid, which has both oxygen absorption ability and carbon dioxide generation ability, as a main ingredient of the oxygen absorption reaction.
Dehydroascorbic acid is a compound obtained by oxidizing ascorbic acid, and produces diketogulonic acid by hydrolysis. By adjusting an appropriate catalyst and reaction environment, decarboxylation and oxidation reactions are repeated to generate carbon dioxide and absorb oxygen. Dehydroascorbic acid can also be produced by oxidizing ascorbic acids.
本発明のガス濃度調整剤において、デヒドロアスコルビン酸は、酸素吸収性能の観点から、水と共に活性炭に含浸していることが好ましい。具体的には、デヒドロアスコルビン酸を水に溶解させたデヒドロアスコルビン酸の水溶液を、多孔性担体である活性炭に含浸させることが好ましい。 In the gas concentration adjusting agent of the present invention, dehydroascorbic acid is preferably impregnated in activated carbon together with water from the viewpoint of oxygen absorption performance. Specifically, it is preferable to impregnate activated carbon as a porous carrier with an aqueous solution of dehydroascorbic acid in which dehydroascorbic acid is dissolved in water.
ガス濃度調整剤においては、デヒドロアスコルビン酸の酸化反応を利用して雰囲気中の酸素を吸収してその濃度を調整すると共に、発生する二酸化炭素を利用して雰囲気中の二酸化炭素濃度を調整する。なお、当該酸化反応においては、理論上、消費された酸素分子と等モル以上の二酸化炭素が生成する。上記の原理のため、酸素濃度を低減させるとそれに伴って二酸化炭素濃度も増加することとなる。 The gas concentration adjusting agent utilizes the oxidation reaction of dehydroascorbic acid to absorb oxygen in the atmosphere and adjusts its concentration, and uses the generated carbon dioxide to adjust the concentration of carbon dioxide in the atmosphere. Note that, in the oxidation reaction, carbon dioxide is theoretically produced in an equimolar amount or more to the consumed oxygen molecules. Due to the above principle, when the oxygen concentration is reduced, the carbon dioxide concentration is also increased accordingly.
(b)アスコルビン酸類
本発明のガス濃度調整剤は、アスコルビン酸類を含んでもよい。アスコルビン酸は、デヒドロアスコルビン酸に比べて低価格で入手しやすく、酸素吸収反応の主剤として酸素吸収能及び炭酸ガス発生能を併せ持つ。
アスコルビン酸類とは、L-アスコルビン酸とその立体異性体並びにその塩及び水和物を意味する。L-アスコルビン酸塩としては、L-アスコルビン酸ナトリウム、L-アスコルビン酸カリウム、L-アスコルビン酸カルシウム等が挙げられる。L-アスコルビン酸の立体異性体としては、エリソルビン酸(D-イソアスコルビン酸)等が挙げられる。エリソルビン酸塩としては、エリソルビン酸ナトリウム、エリソルビン酸カリウム、エリソルビン酸カルシウム等が挙げられる。アスコルビン酸類は、1種単独であってもよく、2種以上を併用してもよい。
(b) Ascorbic Acids The gas concentration adjusting agent of the present invention may contain ascorbic acids. Ascorbic acid is cheaper and more readily available than dehydroascorbic acid, and has both oxygen absorption ability and carbon dioxide generation ability as a main ingredient in the oxygen absorption reaction.
Ascorbic acids refer to L-ascorbic acid, its stereoisomers, salts and hydrates thereof. Examples of L-ascorbate include sodium L-ascorbate, potassium L-ascorbate, calcium L-ascorbate and the like. Stereoisomers of L-ascorbic acid include erythorbic acid (D-isoascorbic acid) and the like. Erythorbate includes sodium erythorbate, potassium erythorbate, calcium erythorbate and the like. One type of ascorbic acid may be used alone, or two or more types may be used in combination.
本発明のガス濃度調整剤において、アスコルビン酸類は、酸素吸収性能の観点から、水と共に活性炭に含浸していることが好ましい。具体的には、アスコルビン酸類を水に溶解させたアスコルビン酸類の水溶液を、多孔性担体である活性炭に含浸させることが好ましい。その際、アスコルビン酸類の水溶液の濃度が高い方が、多孔性担体の使用量を少なくすることができるため、アスコルビン酸類の濃度は、できるだけ飽和溶解度に近い濃度にすることが好ましい。このためアスコルビン酸類としては水に対する溶解度が高い化合物を選択することが好ましい。水に対する溶解度及び入手容易性の観点から、アスコルビン酸類としてはアスコルビン酸又はアスコルビン酸ナトリウムが好ましい。アスコルビン酸又はアスコルビン酸ナトリウムを使用した場合、該水溶液の濃度を40~55質量%とすることが好適である。 In the gas concentration adjusting agent of the present invention, ascorbic acids are preferably impregnated in activated carbon together with water from the viewpoint of oxygen absorption performance. Specifically, it is preferable to impregnate activated carbon as a porous carrier with an aqueous solution of ascorbic acids in which ascorbic acids are dissolved in water. In this case, the higher the concentration of the ascorbic acid aqueous solution, the less the amount of the porous carrier used. Therefore, it is preferable to select a compound having high water solubility as the ascorbic acid. Ascorbic acid or sodium ascorbate is preferable as the ascorbic acid from the viewpoint of solubility in water and availability. When ascorbic acid or sodium ascorbate is used, the concentration of the aqueous solution is preferably 40-55% by mass.
本発明のガス濃度調整剤が(b)アスコルビン酸類を含む場合、(b)アスコルビン酸類と(a)デヒドロアスコルビン酸とのモル比[(b)/(a)]は、好ましくは1.5以下、より好ましくは1.2以下、更に好ましくは1.0以下、更に好ましくは0.7以下、更に好ましくは0.5以下、更に好ましくは0.1以下である。嫌気性細菌の培養の際に、ガスバリア性密閉容器に投入して使用するが、その投入時に上記組成であればよい。 When the gas concentration adjusting agent of the present invention contains (b) ascorbic acids, the molar ratio [(b)/(a)] of (b) ascorbic acids and (a) dehydroascorbic acid is preferably 1.5 or less. , more preferably 1.2 or less, still more preferably 1.0 or less, still more preferably 0.7 or less, still more preferably 0.5 or less, still more preferably 0.1 or less. When culturing anaerobic bacteria, the composition is put into a gas-barrier sealed container and used, and the above composition is sufficient when the container is put.
(c)遷移金属触媒
本発明のガス濃度調整剤は、デヒドロアスコルビン酸及びアスコルビン酸類の酸化反応の進行を促進する遷移金属触媒を含む。
遷移金属触媒は、遷移金属の塩や酸化物等の金属化合物を有する触媒である。遷移金属としては、鉄、マンガン、亜鉛、銅、コバルトが好適である。遷移金属の塩としては、遷移金属のハロゲン化物及び鉱酸塩が含まれ、例えば、遷移金属の塩化物や硫酸塩である。代表例として塩化第一鉄、塩化第二鉄、硫酸第一鉄、硫酸第二鉄、塩化マンガン、硫酸亜鉛、硫酸銅、塩化銅、硫酸コバルトの無水塩又は含水塩等が挙げられ、中でも水への溶解性がよく、配合性が良好な硫酸第一鉄七水和物が好ましい。
(c) Transition Metal Catalyst The gas concentration regulator of the present invention contains a transition metal catalyst that accelerates the oxidation reaction of dehydroascorbic acid and ascorbic acids.
A transition metal catalyst is a catalyst having a metal compound such as a salt or oxide of a transition metal. Preferred transition metals are iron, manganese, zinc, copper and cobalt. Transition metal salts include transition metal halides and mineral salts, such as transition metal chlorides and sulfates. Representative examples include ferrous chloride, ferric chloride, ferrous sulfate, ferric sulfate, manganese chloride, zinc sulfate, copper sulfate, copper chloride, and anhydrous or hydrous salts of cobalt sulfate. Ferrous sulfate heptahydrate is preferred because it has good solubility in water and good blendability.
ガス濃度調整剤中における遷移金属触媒の含有量は、デヒドロアスコルビン酸及びアスコルビン酸類の酸化反応の進行を促進する観点から、デヒドロアスコルビン酸及びアスコルビン酸類の合計100質量部に対して1~30質量部が好ましく、5~25質量部がより好ましく、10~20質量部が更に好ましい。 The content of the transition metal catalyst in the gas concentration adjusting agent is 1 to 30 parts by mass with respect to 100 parts by mass of dehydroascorbic acid and ascorbic acids in total, from the viewpoint of promoting the progress of the oxidation reaction of dehydroascorbic acid and ascorbic acids. is preferred, 5 to 25 parts by weight is more preferred, and 10 to 20 parts by weight is even more preferred.
(d)活性炭
本発明のガス濃度調整剤は活性炭を含む。活性炭は、デヒドロアスコルビン酸水溶液及びアスコルビン酸類水溶液を含浸させる担体としての機能を有するとともに、その比表面積の大きさから空気との接触面積が大きく、酸化反応の進行を促進する機能を有する。
(d) Activated carbon The gas concentration adjusting agent of the present invention contains activated carbon. Activated carbon functions as a carrier for impregnating the aqueous solution of dehydroascorbic acid and the aqueous solution of ascorbic acids, and also has a large specific surface area and a large contact area with air, thereby promoting the progress of the oxidation reaction.
活性炭としては、例えば、おが粉、石炭、椰子殻等を原料として水蒸気賦活、塩化亜鉛等を用いた薬剤賦活等の各種製法で製造されたものを用いることができる。また、活性炭は、デヒドロアスコルビン酸水溶液及びアスコルビン酸類水溶液等を活性炭に担持させ顆粒状で小袋に充填して用いられるために、粒状活性炭が好ましい。粒状活性炭の粒子径は、酸素吸収性能の観点及び包装体への充填性(流動性)の観点から、好ましくは0.1~2mm、より好ましくは0.5~1mmである。 As the activated carbon, for example, those manufactured by using sawdust, coal, coconut shells, etc. as raw materials, steam activation, chemical activation using zinc chloride, etc., can be used. Granular activated carbon is preferable because the activated carbon is used by loading an aqueous solution of dehydroascorbic acid, an aqueous solution of ascorbic acids, etc. on the activated carbon and filling it in a granular form in a sachet. The particle size of the granular activated carbon is preferably 0.1 to 2 mm, more preferably 0.5 to 1 mm, from the viewpoints of oxygen absorption performance and packing properties (fluidity).
ガス濃度調整剤中における活性炭の含有量は、酸素吸収性能の観点及び包装体への充填性の観点から、デヒドロアスコルビン酸及びアスコルビン酸類の合計100質量部に対して50~400質量部が好ましく、75~300質量部がより好ましい。 The content of activated carbon in the gas concentration adjusting agent is preferably 50 to 400 parts by mass with respect to a total of 100 parts by mass of dehydroascorbic acid and ascorbic acids, from the viewpoint of oxygen absorption performance and packing performance, 75 to 300 parts by mass is more preferable.
(e)アルカリ金属炭酸塩、アルカリ金属水酸化物及びアルカリ土類金属水酸化物
本発明のガス濃度調整剤は、アルカリ金属炭酸塩、アルカリ金属水酸化物及びアルカリ土類金属水酸化物からなる群より選ばれる少なくとも1種を含む。アルカリ金属炭酸塩、アルカリ金属水酸化物及びアルカリ土類金属水酸化物からなる群より選ばれる少なくとも1種は、デヒドロアスコルビン酸及びアスコルビン酸類の酸化反応を迅速に進行させ、反応場をアルカリ領域に制御する目的で使用される。
(e) Alkali Metal Carbonate, Alkali Metal Hydroxide and Alkaline Earth Metal Hydroxide The gas concentration adjusting agent of the present invention comprises an alkali metal carbonate, an alkali metal hydroxide and an alkaline earth metal hydroxide. At least one selected from the group is included. At least one selected from the group consisting of alkali metal carbonates, alkali metal hydroxides and alkaline earth metal hydroxides accelerates the oxidation reaction of dehydroascorbic acid and ascorbic acids, and shifts the reaction field to an alkaline region. Used for control purposes.
アルカリ金属炭酸塩としては、炭酸ナトリウム、炭酸水素ナトリウム、炭酸ナトリウム水和物等の、水溶性のアルカリ金属炭酸塩が好適に用いられ、中でも炭酸ナトリウムが特に好ましい。
アルカリ金属水酸化物としては、水酸化カリウム、水酸化ナトリウムが挙げられ、中でも水酸化ナトリウムが好ましい。
アルカリ土類金属水酸化物としては、水酸化カルシウム、水酸化マグネシウムが挙げられる。
As the alkali metal carbonate, water-soluble alkali metal carbonates such as sodium carbonate, sodium hydrogencarbonate and sodium carbonate hydrate are suitably used, with sodium carbonate being particularly preferred.
Examples of alkali metal hydroxides include potassium hydroxide and sodium hydroxide, with sodium hydroxide being preferred.
Alkaline earth metal hydroxides include calcium hydroxide and magnesium hydroxide.
アルカリ金属炭酸塩、アルカリ金属水酸化物及びアルカリ土類金属水酸化物の中でも、アスコルビン酸との塩になったときの水への溶解度の観点から、本発明のガス濃度調整剤は、アルカリ金属炭酸塩及び/又はアルカリ金属水酸化物を含むことが好ましい。
ガス濃度調整剤中におけるアルカリ金属水酸化物の含有量は、加水分解生成物を中和する観点から、デヒドロアスコルビン酸及びアスコルビン酸類の合計モル量に対して等モル量が好ましい。
ガス濃度調整剤中におけるアルカリ金属炭酸塩の含有量は、二酸化炭素濃度を調整する観点から、デヒドロアスコルビン酸及びアスコルビン酸類の合計100質量部に対して10~200質量部が好ましく、50~200質量部がより好ましく、100~150質量部が更に好ましい。
Among alkali metal carbonates, alkali metal hydroxides and alkaline earth metal hydroxides, from the viewpoint of solubility in water when converted to a salt with ascorbic acid, the gas concentration adjuster of the present invention is an alkali metal It preferably contains a carbonate and/or an alkali metal hydroxide.
From the viewpoint of neutralizing hydrolysis products, the content of the alkali metal hydroxide in the gas concentration adjusting agent is preferably equimolar to the total molar amount of dehydroascorbic acid and ascorbic acids.
From the viewpoint of adjusting the carbon dioxide concentration, the content of the alkali metal carbonate in the gas concentration adjusting agent is preferably 10 to 200 parts by mass, and 50 to 200 parts by mass with respect to 100 parts by mass of dehydroascorbic acid and ascorbic acids in total. parts is more preferred, and 100 to 150 parts by mass is even more preferred.
(f)水
本発明のガス濃度調整剤は、デヒドロアスコルビン酸及びアスコルビン酸類の酸化反応の進行に必要な水を含む。
水は、活性炭に含浸させる態様を採ることが、ガス濃度調整剤を流動性のある固形物として得られるという観点から好ましい。本発明のガス濃度調整剤において、水は、酸素吸収性能の観点から、デヒドロアスコルビン酸及びアスコルビン酸類と共に活性炭に含浸していることが好ましい。具体的には、デヒドロアスコルビン酸又はアスコルビン酸類を水に溶解させたデヒドロアスコルビン酸水溶液及びアスコルビン酸類水溶液を、多孔性担体である活性炭に含浸させることが好ましい。また、水には、デヒドロアスコルビン酸及びアスコルビン酸類以外の可溶性成分を溶解させてもよく、不溶性成分を分散させてもよい。
(f) Water The gas concentration adjusting agent of the present invention contains water necessary for the oxidation reaction of dehydroascorbic acid and ascorbic acids to proceed.
It is preferable to impregnate activated carbon with water from the viewpoint of obtaining the gas concentration adjusting agent as a fluid solid matter. In the gas concentration adjusting agent of the present invention, water is preferably impregnated in activated carbon together with dehydroascorbic acid and ascorbic acids from the viewpoint of oxygen absorption performance. Specifically, it is preferable to impregnate activated carbon, which is a porous carrier, with an aqueous solution of dehydroascorbic acid or an aqueous solution of ascorbic acids in which dehydroascorbic acid or an ascorbic acid is dissolved in water. In addition, soluble components other than dehydroascorbic acid and ascorbic acids may be dissolved in water, or insoluble components may be dispersed.
ガス濃度調整剤中における水の含有量は、デヒドロアスコルビン酸及びアスコルビン酸類の酸化反応を進行させる観点から、デヒドロアスコルビン酸及びアスコルビン酸類の合計100質量部に対して、30~500質量部が好ましく、50~300質量部がより好ましく80~200質量部が更に好ましい。 The content of water in the gas concentration adjusting agent is preferably 30 to 500 parts by mass with respect to a total of 100 parts by mass of dehydroascorbic acid and ascorbic acids, from the viewpoint of promoting the oxidation reaction of dehydroascorbic acid and ascorbic acids. 50 to 300 parts by mass is more preferable, and 80 to 200 parts by mass is even more preferable.
(g)その他の成分
本発明のガス濃度調整剤は、本発明の効果を阻害しない範囲内で、上述した(a)~(f)成分以外の成分を必要に応じて含んでもよい。
(g) Other Components The gas concentration adjusting agent of the present invention may optionally contain components other than the components (a) to (f) described above within a range that does not impair the effects of the present invention.
(g1)熱可塑性樹脂
本発明のガス濃度調整剤は、酸素吸収反応(デヒドロアスコルビン酸及びアスコルビン酸類の酸化反応)の進行に伴う過度の発熱を抑制するために、熱可塑性樹脂を含んでもよい。熱可塑性樹脂の種類に特に制限はないが、例えば、ポリエチレン、ポリプロピレン、エチレン-酢酸ビニル共重合体、エラストマー又はこれらの混合物が使用でき、特に分子量10000以下の低分子量ポリエチレン、ポリプロピレン又はこれらの混合物が軟化点の調整が容易であり、臭気の影響が少ないという観点から好適に用いられる。
(g1) Thermoplastic resin The gas concentration adjusting agent of the present invention may contain a thermoplastic resin in order to suppress excessive heat generation accompanying the progress of the oxygen absorption reaction (oxidation reaction of dehydroascorbic acid and ascorbic acids). The type of thermoplastic resin is not particularly limited, but for example, polyethylene, polypropylene, ethylene-vinyl acetate copolymer, elastomer or a mixture thereof can be used, particularly low molecular weight polyethylene having a molecular weight of 10000 or less, polypropylene or a mixture thereof. It is preferably used from the viewpoint that the softening point can be easily adjusted and the influence of odor is small.
熱可塑性樹脂は、他の成分との混合性の観点から、粒子径が1~500μmの粒状体が好ましく、10~300μmの粒状体がより好ましい。また、熱可塑性樹脂の軟化点は、より効果的に発熱を抑制する観点から、90~125℃が好ましい。 The thermoplastic resin preferably has a particle size of 1 to 500 μm, more preferably 10 to 300 μm, from the viewpoint of miscibility with other components. Also, the softening point of the thermoplastic resin is preferably 90 to 125° C. from the viewpoint of suppressing heat generation more effectively.
ガス濃度調整剤中における熱可塑性樹脂の含有量は、デヒドロアスコルビン酸及びアスコルビン酸類の酸化反応を進行させる観点から、デヒドロアスコルビン酸及びアスコルビン酸類の合計100質量部に対して、100~1000質量部が好ましく、300~500質量部がより好ましい。 From the viewpoint of promoting the oxidation reaction of dehydroascorbic acid and ascorbic acids, the content of the thermoplastic resin in the gas concentration adjusting agent is 100 to 1000 parts by mass with respect to a total of 100 parts by mass of dehydroascorbic acid and ascorbic acids. Preferably, 300 to 500 parts by mass is more preferable.
(g2)アルデヒド除去剤
本発明のガス濃度調整剤は、主にデヒドロアスコルビン酸及びアスコルビン酸類の酸化反応の進行に伴って副生するアルデヒドを除去するために、アルデヒド除去剤を含んでもよい。アルデヒド除去能を有する化合物としてはアミン類等、種々のものが公知であるが、アルデヒド除去能が充分であり、刺激臭の発生も見られず、少量で高い効果を発揮するエチレン尿素、尿素、アルギニン、リジン塩酸塩またはポリアリルアミンを配合することが好ましく、より少量で効果の高いエチレン尿素がより好ましい。
(g2) Aldehyde removing agent The gas concentration adjusting agent of the present invention may contain an aldehyde removing agent in order to remove aldehyde that is by-produced mainly with the progress of the oxidation reaction of dehydroascorbic acid and ascorbic acids. Various compounds such as amines are known as compounds having an aldehyde-removing ability. Ethylene urea, urea, Arginine, lysine hydrochloride, or polyallylamine is preferably blended, and ethylene urea, which is more effective in a smaller amount, is more preferable.
本明細書で言うアルデヒドとは、その分子内に1つ以上のホルミル基を有する化合物、すなわち、アルデヒド類を意味する。本発明においては、典型的には、酸素吸収又は細菌培養の過程で副生成分として発生するアルデヒドを意味し、該アルデヒドとしては、細菌培養に悪影響を及ぼす限り化学分野においてアルデヒド類に分類されるものであればいずれのものを包含される。具体的には、例えば、ホルムアルデヒド、アセトアルデヒド等が包含される。 Aldehyde as used herein means a compound having one or more formyl groups in its molecule, that is, aldehydes. In the present invention, it typically means an aldehyde generated as a by-product in the process of absorbing oxygen or culturing bacteria, and the aldehyde is classified as an aldehyde in the chemical field as long as it has an adverse effect on culturing bacteria. Any thing is included if it is a thing. Specifically, for example, formaldehyde, acetaldehyde and the like are included.
ガス濃度調整剤中におけるアルデヒド除去剤の含有量は、アルデヒドを効率的かつ経済的に除去する観点から、デヒドロアスコルビン酸及びアスコルビン酸類の合計100質量部に対して、0.5~25質量部が好ましく、1~10質量部がより好ましく、1~5質量部が更に好ましい。 From the viewpoint of efficiently and economically removing aldehyde, the content of the aldehyde removing agent in the gas concentration adjusting agent is 0.5 to 25 parts by mass with respect to 100 parts by mass of dehydroascorbic acid and ascorbic acids. It is preferably 1 to 10 parts by mass, and even more preferably 1 to 5 parts by mass.
(g3)被覆材
本発明のガス濃度調整剤は、上述した(a)~(f)成分を含む組成物の造粒物の外側に被覆材を有していてもよい。被覆材としては、酸素吸収反応に伴い発生する微量の臭気成分を吸着する観点からは、活性炭、ゼオライト、ケイ酸塩等の多孔質粒子が挙げられる。また、ガス濃度調整剤の流動性を向上し、ガス濃度調整剤を包装材料に充填包装しやすくする観点からは、タルク、ステアリン酸マグネシウム、ステアリン酸カルシウム等が挙げられる。これらの助剤は、1種を単独で用いることができ、又は必要に応じて2種以上を併用して用いることもできる。また、これらの助剤は、市販品を容易に入手することもできる。
(g3) Coating material The gas concentration adjusting agent of the present invention may have a coating material on the outside of the granules of the composition containing the components (a) to (f) described above. Examples of the coating material include porous particles such as activated carbon, zeolite, and silicate, from the viewpoint of adsorbing a small amount of odorous components generated along with the oxygen absorption reaction. Talc, magnesium stearate, calcium stearate and the like can be used from the viewpoint of improving the flowability of the gas concentration adjusting agent and facilitating the filling and packaging of the gas concentration adjusting agent in a packaging material. These auxiliaries can be used singly, or two or more of them can be used in combination, if necessary. In addition, these auxiliaries are readily available commercially.
(ガス濃度調整剤の製造方法)
本発明のガス濃度調整剤の製造方法は、特に制限はないが、例えば、デヒドロアスコルビン酸、遷移金属触媒、アルカリ金属水酸化物等を溶解したデヒドロアスコルビン酸水溶液を調製し、この溶液を活性炭及びアルカリ金属炭酸塩に混合して活性炭に含浸させる方法が挙げられる。また、アスコルビン酸類、遷移金属触媒、アルカリ金属水酸化物等を溶解したアスコルビン酸類水溶液を調製し、一方、デヒドロアスコルビン酸、遷移金属触媒、アルカリ金属水酸化物等を溶解したデヒドロアスコルビン酸水溶液を調製し、これらの溶液を活性炭及びアルカリ金属炭酸塩に混合して活性炭に含浸させる方法も挙げられる。
(Method for producing gas concentration adjusting agent)
The method for producing the gas concentration adjusting agent of the present invention is not particularly limited. A method of mixing with an alkali metal carbonate and impregnating activated carbon can be mentioned. Alternatively, an aqueous ascorbic acid solution is prepared by dissolving ascorbic acids, a transition metal catalyst, an alkali metal hydroxide, etc., and an aqueous dehydroascorbic acid solution is prepared by dissolving dehydroascorbic acid, a transition metal catalyst, an alkali metal hydroxide, etc. Alternatively, a method of mixing these solutions with activated carbon and an alkali metal carbonate and impregnating the activated carbon with the solution is also available.
[ガス濃度調整剤包装体]
ガス濃度調整剤は、上述した各成分を含む組成物を、通気性包装材を全部又は一部に用いた包装材で包装することによって、ガス濃度調整剤包装体とすることもできる。
[Gas concentration adjusting agent package]
The gas concentration adjusting agent can also be made into a gas concentration adjusting agent package by packaging a composition containing each of the components described above in a packaging material that uses an air-permeable packaging material in whole or in part.
(包装材)
包装材としては、2枚の通気性包装材を貼り合わせて袋状としたものや、1枚の通気性包装材と1枚の非通気性包装材とを貼り合わせて袋状としたもの、1枚の通気性包装材を折り曲げ、折り曲げ部を除く縁部同士をシールして袋状としたものが挙げられる。
(packaging material)
As the packaging material, two sheets of air-permeable packaging material are pasted together to form a bag, and one sheet of air-permeable packaging material and one sheet of non-breathable packaging material are pasted together to form a bag-like form, For example, a sheet of air-permeable packaging material is folded, and edges other than the folded portion are sealed to form a bag.
ここで、通気性包装材及び非通気性包装材が四角形状である場合には、包装材は、2枚の通気性包装材を重ね合わせ、4辺をヒートシールして袋状としたものや、1枚の通気性包装材と1枚の非通気性包装材とを重ね合わせ、4辺をヒートシールして袋状としたもの、1枚の通気性包装材を折り曲げ、折り曲げ部を除く3辺をヒートシールして袋状としたものが挙げられる。また包装材は、通気性包装材を筒状にしてその筒状体の両端部および胴部をヒートシールして袋状としたものであってもよい。 Here, when the air-permeable packaging material and the non-air-permeable packaging material have a square shape, the packaging material is a bag-shaped material obtained by stacking two air-permeable packaging materials and heat-sealing the four sides of the packaging material. , A sheet of breathable packaging material and a sheet of non-breathable packaging material are superimposed and heat-sealed on four sides to form a bag, one sheet of breathable packaging material is folded, except for the folded part A case in which the sides are heat-sealed to form a bag is exemplified. Alternatively, the packaging material may be a bag-like material obtained by forming a tubular air-permeable packaging material into a tubular shape and heat-sealing both ends and a trunk portion of the tubular body.
(通気性包装材)
通気性包装材としては、酸素と二酸化炭素を透過する包装材が選択される。なかでも、ガーレ式試験機法による透気抵抗度が600秒以下、より好ましくは90秒以下のものが好適に用いられる。ここで、透気抵抗度とは、JIS P8117(1998)の方法により測定された値を言うものとする。より具体的には、株式会社東洋精機製作所製のガーレ式デンソメーターを使用して100mLの空気が通気性包装材を透過するのに要した時間を言う。
(Breathable packaging material)
As a breathable packaging material, a packaging material that is permeable to oxygen and carbon dioxide is selected. Among them, those having an air resistance of 600 seconds or less, more preferably 90 seconds or less, as measured by the Gurley tester method, are preferably used. Here, the air resistance means a value measured by the method of JIS P8117 (1998). More specifically, it refers to the time required for 100 mL of air to permeate the air-permeable packaging material using a Gurley densometer manufactured by Toyo Seiki Seisakusho.
上記通気性包装材としては、紙や不織布の他、プラスチックフィルムに通気性を付与したものが用いられる。プラスチックフィルムとしては、例えば、ポリエチレンテレフタレート、ポリアミド、ポリプロピレン、ポリカーボネート等のフィルムと、シール層としてポリエチレン、アイオノマー、ポリブタジエン、エチレン/アクリル酸コポリマー、エチレン/メタクリル酸コポリマー又はエチレン/酢酸ビニルコポリマー等のフィルムとを積層接着した積層フィルム等が使用できる。また、これらの積層物も通気性包装材として使用することができる。 As the air-permeable packaging material, paper, non-woven fabric, and plastic film with air permeability are used. Examples of plastic films include films such as polyethylene terephthalate, polyamide, polypropylene, and polycarbonate, and films such as polyethylene, ionomer, polybutadiene, ethylene/acrylic acid copolymer, ethylene/methacrylic acid copolymer, and ethylene/vinyl acetate copolymer as sealing layers. can be used. These laminates can also be used as breathable packaging materials.
通気性を付与する方法としては、冷針、熱針による穿孔加工の他、種々の方法が採用可能である。穿孔加工により通気性を付与する場合、通気性は、穿孔する孔の径、数、材質等により自由に調整することができる。 As a method for imparting air permeability, various methods such as perforation using cold needles and hot needles can be employed. When air permeability is imparted by perforation, the air permeability can be freely adjusted by the diameter, number, material, etc. of the holes to be perforated.
また、積層フィルムの厚さは、50~300μmであることが好ましく、60~250μmであることが特に好ましい。この場合、厚さが上記範囲を外れる場合に比べて、強度を保持しヒートシール性や包装適性に優れた包装材とすることができる。 Also, the thickness of the laminated film is preferably 50 to 300 μm, particularly preferably 60 to 250 μm. In this case, compared with the case where the thickness is outside the above range, the packaging material can be made to have strength, heat-sealing property, and packaging suitability.
上記のガス濃度調整剤包装体はその機能を長期間維持するため、使用前はガスバリア性の容器や袋に収納し、使用するにあたりガスバリア性の容器や袋から取り出して用いることが好ましい。また、菌培養の用途にガス濃度調整剤包装体を使用する際は、該包装体に対して予めγ線等を用いた殺菌を施すことが好ましい。 In order to maintain the function of the gas concentration adjusting agent package for a long period of time, it is preferable to store it in a gas-barrier container or bag before use and remove it from the gas-barrier container or bag before use. Further, when the gas concentration adjusting agent package is used for bacterial culture, it is preferable to sterilize the package in advance using γ-rays or the like.
[嫌気性細菌の培養方法]
本発明の嫌気性細菌の培養方法は、ガス濃度調整剤の存在下で嫌気性細菌を培養する方法である。具体的には、嫌気性細菌及び培地を収容した培養容器と共にガス濃度調整剤(好ましくはガス濃度調整剤包装体)を、ガスバリア性密閉容器内に設置後、密封し、該密閉容器を細菌培養に好適な温度下に静置することで実施できる。
[Method for culturing anaerobic bacteria]
The method for culturing anaerobic bacteria of the present invention is a method for culturing anaerobic bacteria in the presence of a gas concentration adjusting agent. Specifically, a culture container containing anaerobic bacteria and a culture medium and a gas concentration adjusting agent (preferably a gas concentration adjusting agent package) are placed in a gas barrier closed container, then sealed, and the closed container is used for bacterial culture. It can be carried out by standing under a temperature suitable for.
本発明の培養方法に用いられる培地については特に制限はなく、一般的に使用されているものがそのまま適用できるため、培養する菌に適した培地を自由に選択できる。培地中に溶け込むアルデヒド濃度は、好ましくは2mg/L以下、より好ましくは1.5mg/L以下、更に好ましくは1.0mg/L以下とするのが、菌培養条件として好適である。
また、培養温度は20~45℃であることが好ましく、25~40℃であることが特に好ましい。
The medium used in the culture method of the present invention is not particularly limited, and commonly used media can be applied as they are. The concentration of aldehyde dissolved in the medium is preferably 2 mg/L or less, more preferably 1.5 mg/L or less, and still more preferably 1.0 mg/L or less, as conditions for bacterial culture.
Also, the culture temperature is preferably 20 to 45°C, particularly preferably 25 to 40°C.
培養容器は、容器外との通気性が確保されていれば特に制限はなく、容積、形状、材質等いずれも培養に適した任意のものを採用することができる。蓋部を有する培養容器が好ましく用いられるが、この際も、容器外との通気性を確保する必要がある。 The culture vessel is not particularly limited as long as air permeability with the outside of the vessel is ensured, and any volume, shape, material, etc. suitable for culture can be adopted. A culture vessel having a lid is preferably used, but even in this case, it is necessary to ensure air permeability with the outside of the vessel.
本発明の細菌の培養方法は、嫌気性細菌の培養に適用される。本発明の培養方法においては、培養実施前のガスバリア性密閉容器内の雰囲気は特に限定されず空気であってもよいが、嫌気性細菌を培養する観点から、窒素雰囲気であることが好ましい。 The method for culturing bacteria of the present invention is applied to culturing anaerobic bacteria. In the culture method of the present invention, the atmosphere in the gas-barrier sealed container before culture is not particularly limited and may be air, but from the viewpoint of culturing anaerobic bacteria, a nitrogen atmosphere is preferred.
細菌培養方法で用いられるガスバリア性密閉容器は、その内外の気体の流通を妨げ、投入したガス濃度調整剤により形成された酸素、二酸化炭素濃度を長期間維持するものである。ガラス、金属、ポリカーボネート等のプラスチック等で構成された容器がよく用いられるが、ガスバリア性フィルム及びその積層物を使用することも可能である。 The gas-barrier sealed container used in the bacterial culture method prevents the flow of gas inside and outside the container, and maintains for a long period of time the concentrations of oxygen and carbon dioxide formed by the introduced gas concentration adjusting agent. Containers made of glass, metal, plastic such as polycarbonate, etc. are often used, but gas barrier films and laminates thereof can also be used.
この際、ガスバリア性密閉容器内で発生したアルデヒドの発生量を測定することや該容器内の湿度の調整等を目的として、該密閉容器内に蒸留水を収容した開放型の容器を設置してもよい。開放型の容器としては培養容器の他、ビーカー、フラスコ等が例示でき、細菌及び培地を収容した培養容器と同種の容器であることが好ましい。 At this time, for the purpose of measuring the amount of aldehyde generated in the gas-barrier closed container and adjusting the humidity in the container, an open container containing distilled water was placed in the closed container. good too. Examples of the open-type container include a culture container, a beaker, a flask, and the like, and the same type of container as the culture container containing the bacteria and medium is preferable.
嫌気性細菌を培養する観点から、密閉容器内の酸素濃度は、24時間以内で0.1容量%以下になることが好ましい。また、密閉容器内の二酸化炭素濃度は、11.5容量%以上が好ましく、12容量%以上がより好ましく、13容量%以上が更に好ましく、15容量%以上が更に好ましい。 From the viewpoint of culturing anaerobic bacteria, it is preferable that the oxygen concentration in the closed container becomes 0.1% by volume or less within 24 hours. Also, the carbon dioxide concentration in the sealed container is preferably 11.5% by volume or more, more preferably 12% by volume or more, still more preferably 13% by volume or more, and even more preferably 15% by volume or more.
細菌培養においては、短時間で所望の酸素濃度及び二酸化炭素濃度にすることが重要となる。嫌気性細菌を培養する観点から、デヒドロアスコルビン酸及びアスコルビン酸類の酸化反応の反応初期(反応開始から3時間後)の酸素濃度は、0.50容量%以下が好ましく、0.30容量%以下がより好ましく、0.15容量%以下がより好ましい。デヒドロアスコルビン酸及びアスコルビン酸類の酸化反応の反応初期(反応開始から3時間後)の二酸化炭素濃度は、11.5容量%以上が好ましく、12容量%以上がより好ましく、13容量%以上が更に好ましく、15容量%以上が更に好ましい。 In bacterial culture, it is important to reach the desired oxygen concentration and carbon dioxide concentration in a short period of time. From the viewpoint of culturing anaerobic bacteria, the oxygen concentration at the beginning of the oxidation reaction of dehydroascorbic acid and ascorbic acids (3 hours after the start of the reaction) is preferably 0.50% by volume or less, and 0.30% by volume or less. More preferably, it is 0.15% by volume or less. The carbon dioxide concentration at the initial stage of the oxidation reaction of dehydroascorbic acid and ascorbic acids (3 hours after the start of the reaction) is preferably at least 11.5% by volume, more preferably at least 12% by volume, and even more preferably at least 13% by volume. , more preferably 15% by volume or more.
本発明の培養方法によれば、ガスボンベ及びガスコントローラーを使用することなく、好適なガス雰囲気下での細菌の顕微鏡観察や輸送を可能にする。 According to the culture method of the present invention, bacteria can be microscopically observed and transported under a suitable gas atmosphere without using a gas cylinder and a gas controller.
以下、実施例及び比較例を用いて本実施形態を詳しく説明するが、本実施形態は本発明の作用効果を奏する限りにおいて適宜変更することができる。なお、実施例及び比較例中の「部」は、特に明記しない場合は質量部を意味する。 The present embodiment will be described in detail below using examples and comparative examples, but the present embodiment can be modified as appropriate as long as the effects of the present invention are exhibited. "Parts" in Examples and Comparative Examples means parts by mass unless otherwise specified.
製造例1
(アスコルビン酸水溶液の調製)
窒素雰囲気下、L-アスコルビン酸30.6g、15質量%水酸化ナトリウム水溶液46.2g、硫酸第一鉄・七水和物4.8gを混合し、2.13mmol/gのアスコルビン酸水溶液を調製した。
Production example 1
(Preparation of ascorbic acid aqueous solution)
Under a nitrogen atmosphere, 30.6 g of L-ascorbic acid, 46.2 g of 15% by mass sodium hydroxide aqueous solution, and 4.8 g of ferrous sulfate heptahydrate are mixed to prepare a 2.13 mmol/g ascorbic acid aqueous solution. bottom.
製造例2
(デヒドロアスコルビン酸水溶液の調製)
窒素雰囲気下、デヒドロアスコルビン酸4.5g、15質量%水酸化ナトリウム水溶液6.9g、硫酸第一鉄・七水和物0.7gを混合し、2.13mmol/gのデヒドロアスコルビン酸水溶液を調製した。
Production example 2
(Preparation of dehydroascorbic acid aqueous solution)
Under a nitrogen atmosphere, 4.5 g of dehydroascorbic acid, 6.9 g of 15% by mass sodium hydroxide aqueous solution, and 0.7 g of ferrous sulfate heptahydrate are mixed to prepare a 2.13 mmol/g dehydroascorbic acid aqueous solution. bottom.
実施例1
窒素雰囲気下、活性炭10g、ポリエチレン粉末15g、炭酸ナトリウム4.7gを測り取り混合した。この粉体に、アスコルビン酸水溶液10.1g、デヒドロアスコルビン酸水溶液10.1gを添加して混合し、脱酸素剤組成物を製造した。この脱酸素剤組成物6.9gをアルミニウム袋に充填し封止をした。
上記の脱酸素剤を入れたアルミニウム袋をナイロン袋に空気750mLとともに封入し、ナイロン袋内でアルミニウム袋を開封して、脱酸素実験を開始した。3時間後の酸素濃度及び二酸化炭素濃度をガスクロマトグラフで測定したところ、酸素濃度が0.20容量%、二酸化炭素濃度が13.6容量%であった。また、24時間後の酸素濃度及び二酸化炭素濃度をガスクロマトグラフで測定したところ、酸素濃度が0.00容量%、二酸化炭素濃度が13.7容量%であった。
Example 1
In a nitrogen atmosphere, 10 g of activated carbon, 15 g of polyethylene powder, and 4.7 g of sodium carbonate were measured and mixed. To this powder, 10.1 g of an aqueous ascorbic acid solution and 10.1 g of an aqueous dehydroascorbic acid solution were added and mixed to produce an oxygen absorber composition. An aluminum bag was filled with 6.9 g of this oxygen absorber composition and sealed.
An aluminum bag containing the oxygen scavenger was enclosed in a nylon bag together with 750 mL of air, and the aluminum bag was opened in the nylon bag to start a deoxidation experiment. When the oxygen concentration and carbon dioxide concentration after 3 hours were measured with a gas chromatograph, the oxygen concentration was 0.20% by volume and the carbon dioxide concentration was 13.6% by volume. Further, when the oxygen concentration and carbon dioxide concentration after 24 hours were measured with a gas chromatograph, the oxygen concentration was 0.00% by volume and the carbon dioxide concentration was 13.7% by volume.
実施例2
窒素雰囲気下、活性炭10g、ポリエチレン粉末15g、炭酸ナトリウム4.7gを測り取り混合した。この粉体に、デヒドロアスコルビン酸水溶液20.3gを添加して混合し、脱酸素剤組成物を製造した。この脱酸素剤組成物6.9gをアルミニウム袋に充填し封止をした。
上記の脱酸素剤を入れたアルミニウム袋をナイロン袋に空気750mLとともに封入し、ナイロン袋内でアルミニウム袋を開封して、脱酸素実験を開始した。3時間後の酸素濃度及び二酸化炭素濃度をガスクロマトグラフで測定したところ、酸素濃度が0.10容量%、二酸化炭素濃度が18.5容量%であった。また、24時間後の酸素濃度及び二酸化炭素濃度をガスクロマトグラフで測定したところ、酸素濃度が0.00容量%、二酸化炭素濃度が18.6容量%であった。
Example 2
In a nitrogen atmosphere, 10 g of activated carbon, 15 g of polyethylene powder, and 4.7 g of sodium carbonate were measured and mixed. To this powder, 20.3 g of dehydroascorbic acid aqueous solution was added and mixed to produce an oxygen absorber composition. An aluminum bag was filled with 6.9 g of this oxygen absorber composition and sealed.
An aluminum bag containing the oxygen scavenger was enclosed in a nylon bag together with 750 mL of air, and the aluminum bag was opened in the nylon bag to start a deoxidation experiment. When the oxygen concentration and carbon dioxide concentration after 3 hours were measured with a gas chromatograph, the oxygen concentration was 0.10% by volume and the carbon dioxide concentration was 18.5% by volume. Further, when the oxygen concentration and carbon dioxide concentration after 24 hours were measured with a gas chromatograph, the oxygen concentration was 0.00% by volume and the carbon dioxide concentration was 18.6% by volume.
比較例1
窒素雰囲気下、活性炭10g、ポリエチレン粉末15g、炭酸ナトリウム4.7gを測り取り混合した。この粉体に、アスコルビン酸水溶液20.3gを添加して混合し、脱酸素剤組成物を製造した。この脱酸素剤組成物6.9gをアルミニウム袋に充填し封止をした。
上記の脱酸素剤を入れたアルミニウム袋をナイロン袋に空気750mLとともに封入し、ナイロン袋内でアルミニウム袋を開封して、脱酸素実験を開始した。3時間後の酸素濃度及び二酸化炭素濃度をガスクロマトグラフで測定したところ、酸素濃度が0.55容量%、二酸化炭素濃度が10.7容量%であった。また、24時間後の酸素濃度及び二酸化炭素濃度をガスクロマトグラフで測定したところ、酸素濃度が0.00容量%、二酸化炭素濃度が11.0容量%であった。
Comparative example 1
In a nitrogen atmosphere, 10 g of activated carbon, 15 g of polyethylene powder, and 4.7 g of sodium carbonate were measured and mixed. To this powder, 20.3 g of an aqueous ascorbic acid solution was added and mixed to produce an oxygen absorber composition. An aluminum bag was filled with 6.9 g of this oxygen absorber composition and sealed.
An aluminum bag containing the oxygen scavenger was enclosed in a nylon bag together with 750 mL of air, and the aluminum bag was opened in the nylon bag to start a deoxidation experiment. When the oxygen concentration and the carbon dioxide concentration after 3 hours were measured with a gas chromatograph, the oxygen concentration was 0.55% by volume and the carbon dioxide concentration was 10.7% by volume. Further, when the oxygen concentration and the carbon dioxide concentration after 24 hours were measured with a gas chromatograph, the oxygen concentration was 0.00% by volume and the carbon dioxide concentration was 11.0% by volume.
Claims (5)
(b)アスコルビン酸類を含まないか、(b)アスコルビン酸類を更に含み、(b)アスコルビン酸類と(a)デヒドロアスコルビン酸とのモル比[(b)/(a)]が1.5以下である、嫌気性細菌培養用ガス濃度調整剤。 (e) at least one selected from the group consisting of alkali metal carbonates, alkali metal hydroxides and alkaline earth metal hydroxides, (a) dehydroascorbic acid, (c) a transition metal catalyst, (d) activated carbon , and (f) water,
(b) does not contain ascorbic acids, or (b) further contains ascorbic acids, and the molar ratio [(b)/(a)] of (b) ascorbic acids and (a) dehydroascorbic acid is 1.5 or less A gas concentration regulator for anaerobic bacteria culture.
Priority Applications (6)
| Application Number | Priority Date | Filing Date | Title |
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| JP2019116715A JP7322545B2 (en) | 2019-06-24 | 2019-06-24 | Gas concentration adjusting agent for culturing anaerobic bacteria and method for culturing anaerobic bacteria using the same |
| US17/619,799 US12297420B2 (en) | 2019-06-24 | 2020-06-08 | Agent for regulating concentration of gas for anaerobic bacterium culture and method for culturing anaerobic bacterium using same |
| KR1020217040872A KR102903422B1 (en) | 2019-06-24 | 2020-06-08 | Gas concentration regulator for culturing anaerobic bacteria and method for culturing anaerobic bacteria using the same |
| PCT/JP2020/022460 WO2020261951A1 (en) | 2019-06-24 | 2020-06-08 | Agent for regulating concentration of gas for anaerobic bacterium culture and method for culturing anaerobic bacterium using same |
| CN202080043478.6A CN114127257B (en) | 2019-06-24 | 2020-06-08 | Gas concentration regulator for anaerobic bacteria culture and anaerobic bacteria culture method using the same |
| EP20833575.2A EP3988638A4 (en) | 2019-06-24 | 2020-06-08 | MEANS OF CONTROLLING GAS CONCENTRATION FOR ANAEROBIC BACTERIA CULTURE AND METHOD OF CULTIVATION OF ANAEROBIC BACTERIUM USING THE SAME |
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| DE3276537D1 (en) * | 1982-12-21 | 1987-07-16 | Toppan Printing Co Ltd | Culture of anaerobic bacteria |
| JP2666323B2 (en) * | 1988-02-08 | 1997-10-22 | 凸版印刷株式会社 | Oxygen absorber for anaerobic bacteria culture |
| JP3818324B2 (en) | 1996-03-26 | 2006-09-06 | 三菱瓦斯化学株式会社 | Gas concentration adjusting agent and method for adjusting low oxygen concentration environment |
| DE69818893T2 (en) * | 1997-04-01 | 2004-05-19 | Mitsubishi Gas Chemical Co., Inc. | Culture atmosphere regulator and method for growing anaerobic bacteria |
| JPH10327845A (en) * | 1997-04-01 | 1998-12-15 | Mitsubishi Gas Chem Co Inc | Atmosphere regulator and anaerobic bacteria culture method |
| US9085752B2 (en) | 2009-11-24 | 2015-07-21 | Mitsubishi Gas Chemical Company, Inc. | Atmosphere control composition |
| JP2014023541A (en) * | 2013-11-06 | 2014-02-06 | Mitsubishi Gas Chemical Co Inc | Atmosphere-regulating agent and method for culturing cell by using the same |
| US10723992B2 (en) | 2015-04-29 | 2020-07-28 | 3M Innovative Properties Company | Thin film culture device with carbon dioxide generant |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| KR20060118908A (en) | 2005-05-17 | 2006-11-24 | 주식회사종근당 | Liquid composition of vitamin C containing carbon dioxide |
| JP2012076046A (en) | 2010-10-04 | 2012-04-19 | Kyodo Printing Co Ltd | Cysteine-based oxygen absorbent |
| WO2018101944A1 (en) | 2016-12-01 | 2018-06-07 | Multisorb Technologies, Inc. | Oxygen absorbing and carbon dioxide emitting composition |
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| KR20220024030A (en) | 2022-03-03 |
| EP3988638A1 (en) | 2022-04-27 |
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